[0001] This invention relates to a method for preparing a novel class of fluorinated polyorganosiloxanes.
The copolymers effectively stabilize the structure of partially cured foams prepared
from moisture curable RTV polyorganosiloxane compositions.
[0002] Room temperature vulcanizable (RTV) polyorganosiloxane foams have been obtained by
introducing a blowing agent into a one-part moisture curable RTV elastomeric composition.
These types of compositions are well known, and are typically prepared by mixing together,
in the absence of atmospheric moisture, at least one hydroxyl endblocked polydiorganosiloxane
and at least one silane or siloxane containing three or more silicon-bonded hydrolyzable
groups such as carboxyl, alkoxy, ketoximo, amido or aminoxy. The compositions can
also include curing catalysts, fillers, adhesion promoters, pigments, flame retardants
and other additives to modify the appearance and/or the properties of the cured elastomer.
[0003] A disadvantage of employing moisture curable RTV compositions for preparing foams
is the relatively long time period required for the composition to cure to the extent
that the foam becomes self supporting. Once the expansion due to the action of the
blowing agent is substantially completed, the partially cured foam begins to collapse.
In addition, liquid material drains from the foam and eventually forms a layer of
solid rubber beneath the foam. The relatively high density of the resultant foams
and the presence of appreciable amounts of solid rubber may more than offset the advantages
of utilizing these foams for insulation, cushioning and other typical foam applications.
[0004] The problem of maintaining the structure of moisture curable polyorganosiloxane foams
during curing has been addressed by F. Modic and B. Boudreau in U. S. Patent No. 4,368,279,
which issued on January 11, 1983. Modic and Boudreau teach maintaining the initially
produced foam under a vacuum of at least 600 mm of mercury for the time required for
the foam to become self supporting. The one example of a moisture curable RTV composition
in this patent discloses that following vigorous stirring of the composition, ambient
pressure was gradually reduced to 10 mm of mercury over a period of 2 to 5 minutes
and maintained at this level for 10 minutes.
[0005] While the application of vacuum to a foam during curing may be feasible for the formation
of slab stock using a foam machine, it requires specialized equipment including vacuum
pumps and a substantially air-tight chamber for preparing the foam. The use of vacuum
would not be practical, or in some instances even feasible, if the foam is prepared
at the location where it is to be installed, which can be at relatively remote sites.
In such situations, it would be far more desirable to have all of the ingredients
required to prepare the foam, including a blowing agent, packaged in a single container
such as an aerosol can.
[0006] Foamable one-package RTV elastomeric compositions are disclosed in German Patent
Publications 2,909,443 (published September 18, 1980) and 2,911,971 (published October
4, 1980), both of which are assigned to Perrenatorwerk Alfred Hagen GmbH. The compositions
include a low boiling solvent and/or a compressed gas as the blowing agent and are
packaged in a flexible container that is equipped with a valve. The container forms
one part of a 2-compartment pressurizable dispensing package. The second compartment
contains a compressed gas that supplies the pressure required to dispense the RTV
composition from the package. In the exemplified composition, enough gas diffuses
through the wall of the flexible container to act as a blowing agent for the foamable
composition. The composition contains 50% by weight of chalk and 4% by weight of silica.
This amount of filler is required to maintain the structure of the foam during curing,
however the density of the cured foam is very high due to the large amount of filler
present. U.S. Patent No. 4,229,548, which issued on October 21, 1980 to Sattlegger
et al. discloses RTV compositions similar to those disclosed in the foregoing German
patent publications, but teaches using pressurizable containers equipped with nonpermeable,
flexible inner containers for the foamable compositions.
[0007] The prior art discloses additives for reducing the density of polyorganosiloxane
foams prepared by the reaction of polydiorganosiloxanes containing silicon-bonded
hydroxyl groups with curing agents containing silicon-bonded hydrogen atoms. United
States Patent No. 4,026,845, which issued to Y. K. Kim et al. on May 31, 1977, teaches
known fluorine-containing surfactants for this purpose. The surfactants contain fluorinated
carbon atoms, and include both organic and organosilicon compounds.
[0008] United States Patent No. 3,511,788, which issued to J. Keil on May 12, 1970, discloses
using a foam stabilizer to prepare foams from (1) organic liquids having surface tension
values in contact with air at 25°C of at least 2.2 x 10 newtons per centimeter, or
(2) organic plastisols containing a plasticizer and a vinyl resin such as polyvinyl
chloride. The foam stabilizer is an organosiloxane copolymer containing SiO
4/2 units and units selected from (CH
3)
3SiO
1/2 and Q(CH
3)
2SiO
1/4 where Q is defined as a "solubilizing" group that makes the copolymer at least partially
compatible with the organic liquid or plastisol to be foamed. The patent teaches that
examples of solubilizing groups that can be employed in the Q radical include carboxyl,
ester, amide, amino, mercapto, halocarbon, nitrile, nitro, carbonyl and "higher hydrocarbon
groups." Fluorocarbon groups are not specifically disclosed. Because polydimethylsiloxanes
typically exhibit surface tension values below 2.2 x 10-4 newtons per centimeter,
using these polydimethylsiloxanes as a foamable material in combination with a foam
stabilizer disclosed in the aforementioned Keil patent would be outside the scope
of the invention defined in this patent.
[0009] United States Patent No. 3,328,349, which issued to Charles Lentz on June 27, 1967,
discloses benzene soluble copolymers consisting essentially of (C
nF
2n+1CH
2CH
2) (CH
3)
2SiO
0.5 units, where n has a value of from 1 to 10, and Si04/2 units. An average of from
0.3 to 1.0 fluorine-containing siloxane units are present per SiO
4/2 unit. Lentz teaches that the disclosed copolymers are useful defoaming agents. On
the basis of this teaching, copolymers of the type disclosed by Lentz would not be
considered likely candidates to stabilize the structure of partially cured polyorganosiloxane
foams.
[0010] The present invention is based on the discovery that a novel class of resinous organosiloxane
copolymers containing trimethylsiloxy and fluorinated organosiloxy groups in addition
to SiO
4/2 and silicon-bonded hydroxyl groups can be prepared by reacting silanes containing
fluorinated hydrocarbon radicals bonded to silicon by a -CH
2CH
2- radical with organosiloxane copolymers containing trimethylsiloxy units, SiO
4/2 units and silicon-bonded hydroxyl groups.
[0011] The resinous benzene-soluble organosiloxane copolymers prepared using the present
method consist essentially of (a) repeating units of the formulae Sio
4/2; R(CH
3)
2SiO
1/2; and units of the general formula R'CH
2CH
2Si (R')
n°
(3-n)/2 where R represents a saturated or ethylenically unsaturated hydrocarbon radical containing
from 1 to 4 carbon atoms or a phenyl radical, R' represents a monovalent organic group
containing at least 4 perfluorinated carbon atoms, R" represents an alkyl radical
containing from 1 to 3 carbon atoms or a phenyl radical and n is 0, 1 or 2; (b) silicon-bonded
hydroxyl groups and, optionally (c) (CH
3)
2SiO units. The molar ratio of all units in the copolymer other than silicon-bonded
hydroxyl groups and SiO
4/2 units to said SiO
4/2 units is from 0.7:1 to 1.1:1, inclusive, and the concentration of silicon-bonded
hydroxyl groups in said copolymer is from 0 to 4.0% by weight.
[0012] In preferred embodiments of the present copolymers, R is methyl and the molar ratio
of (CH
3)
3SiO
1/2 units to said fluorine-containing units is such that
(a) the surface tension exhibited by a 10% by weight solution of the copolymer in
a hydroxyl endblocked polydimethylsiloxane exhibiting a viscosity of 0.08 Pa's at
25°C is less than 2.2 x 10 -4 newtons per cm at 25°C when in contact with air, and
(b) optical clarity is achieved by the addition to said solution of from 0 to 100
percent by weight of o-xylene.
[0013] These copolymers are claimed in an application for Letters Patent entitled "Novel
Fluorinated Organosiloxane Copolymers" that is being filed concurrently herewith in
the names of Chi-Long Lee, Thomas Fay-Oy Lim and Antony Pope Wright.
[0014] This invention provides a method for preparing the aforementioned novel fluorinated
organosiloxane copolymers, said method comprising the steps of (I) heating at a temperature
of from 50°C to the boiling point thereof a liquid reaction mixture comprising, (A)
a fluorinated silane of the formula R'CH2CH2Si(R')nX3-n; (B) a nonfluorinated benzene
soluble organosiloxane copolymer comprising repeating units of the formulae R(CH
3)SiO
1/2, and SiO
1/2 in a molar ratio of from 0.6:1 - 1.1:1, respectively, and at least 0.1% by weight
of silicon-bonded hydroxyl groups; (II) continuing heating of said liquid reaction
mixture for a period sufficient to form said fluorine-containing organosiloxane copolymer,
and (III) removing any acidic by products generated during the reaction of (A) and
(B), where R, R' R''' and n are as defined hereinabove and X represents a hydrolyzable
group.
[0015] The hydrocarbon radical represented by R can be saturated or ethylenically unsaturated
and contains from 1 to 4 carbon atoms. R can be, for example, methyl, ethyl, vinyl,
allyl or propyl. Alternatively, R can be phenyl.
[0016] The fluorinated organic group represented by R in the foregoing formula contains
at least 4 perfluorinated carbon atoms, and can also include partially fluorinated
and nonfluorinated carbon atoms. The atoms that constitute the R' groups can be present
as linear chains, branched chains or as carbocyclic rings that may contain one or
more double bonds between adjacent carbon atoms. The fluorinated carbon atoms can
be adjacent to one another or separated by nonfluorinated carbon atoms, atoms such
as nitrogen, oxygen or sulfur, or by divalent groups such as carbonyl, amido, carboalkoxy,
sulfonamido and other groups that do not hydrolyze readily in the presence of atmospheric
moisture, or under the reaction conditions employed to prepare the organosiloxane
copolymers of this invention. R' can contain from 4 to 20 or more carbon atoms. Preferably
R' contains from 4 to 16 carbon atoms.
[0017] The molar ratio of units other than hydroxyl and SiO
4/2 to the SiO
4/2 units in the present copolymers is from 0.7:1 to 1.1:1, inclusive. For preferred
embodiments, that are particularly effective polyorganosiloxane foam stabilizers,
this ratio is from 0.7:1 to 0.9:1, inclusive.
[0018] The present copolymers can be prepared by reacting a fluorinated silane (A) of the
general formula R'CH
2CH
2Si(R')
nX
3-n' where R', R", X and n are as previously defined, with a nonfluorinated organosiloxane
copolymer (B) described hereinbefore. These copolymers can optionally contain up to
about 10 mole percent, based on Si04/2 units, of R
2SiO units.
[0019] The group represented by X in the foregoing formula for (A) can be a halogen atom,
such as chlorine, or a hydrolyzable group such as alkoxy, amido or acyloxy. Preferably
X is halogen, based on the availability of these silanes.
[0020] Copolymers of the type useful as (B) and methods for their preparation are described
in United States Patent No. 2,676,182, which issued to Daudt and Tyler on April 20,
1954. This patent teaches organosiloxane copolymers suitable as reactant (B) for preparing
the present copolymers. In accordance with Daudt and Tyler's teaching, a silica hydrosol
is neutralized using a chlorosilane or the combination of sufficient acid to achieve
a pH of 5 or less with either an alkoxysilane or a siloxane. The organosilicon layer
of the resultant two-phase composition is then washed free of acid and dried to yield
the final product as a viscous oil or thermoplastic resin, depending upon the organic
groups present on the organosilicon reactant.
[0021] Reactant (A), a fluorinated silane or a partial hydrolysate thereof can be prepared
by hydrosilation of a fluoroolefin of the formula R'CH=CH
2 with a substantially equimolar quantity of a hydrogen-containing nonfluorinated silane
of the formula HSi(R" )
nX
3-n' where R" and X are defined hereinbefore. Preferably R'' is methyl or phenyl, based
on availability of these silanes. Most preferably R" is methyl.
[0022] As disclosed hereinbefore, the radical represented by R' in the formulae for the
fluoroolefin and reactant (A) is a monovalent organic radical containing at least
four perfluorinated carbon atoms. Partially fluorinated or nonfluorinated carbon atoms
can be present so long as R contains at least four perfluorinated carbon atoms.
[0023] Fluoroolefins containing a variety of fluorocarbon radicals corresponding to R' in
the foregoing formulae are commercially available or can be synthesized with a minimum
of experimentation using procedures disclosed in patents and other published literature.
R' preferably represents F(C
mF
2m, based on the availability of this type of fluoroolefin, and m has an average value
from 4 up to 20 or more, inclusive.
[0024] One particularly preferred type of fluoroolefin is available from E. I. DuPont deNemours
and Co., Wilmington, Delaware, as a mixture of homologous compounds exhibiting the
average formula F(CF
2)
pCH=CH
2, where p is an even integer from 6 to 14, inclusive in each of the fluoroolefin molecules.
Typically, homologs where p is 6, 8, 10 and 12 constitute at least 95% by weight of
the mixture. Some samples of this type of olefin may contain sufficient iodine to
interfere with a hydrosilation reaction. In such instances, it is often desirable
to remove at least a portion of the iodine by refluxing the olefin over finely divided
metallic zinc and distilling it prior to reacting it with the hydrogen-containing
silane.
[0025] Hydrosilation reactions are typically conducted at temperatures of from about 90
to about 300°C using a platinum group metal, a compound thereof, such as chloroplatinic
acid, or an organic peroxide as the catalyst. The hydrosilation of fluorinated olefins
is disclosed in United States Patent No. 3,620,992, which issued to Kim and Pierce
on November 16, 1971 and teaches a general method for preparing fluorosilanes.
[0026] The hydrosilation reaction between any of the fluoroolefins described hereinabove
and the hydrogen-containing silane HSi(R")
nX
3-n can be conducted using substantially equimolar amounts of the two reactants, based
on the average molecular weight of the fluoroolefin. In some instances, a higher yield
of fluorosilane can be obtained by conducting the reaction under superatmospheric
pressure in a sealed vessel, such as a glass tube or autoclave, which is heated at
temperatures of from 90° to 250°C for several hours. This is particularly true if
the fluoroolefin or silane contains impurities that inhibit or otherwise adversely
affect the activity of the hydrosilation catalyst.
[0027] The fluorinated silane (A) obtained from the hydrosilation reaction is reacted with
the organosiloxane copolymer (B) described hereinbefore. The content of silicon-bonded
hydroxyl groups in (B) is preferably from 2 to 7%, based on the weight of the copolymer.
Because the copolymer is a resinous solid at ambient temperature, it is preferably
dissolved in a liquid aromatic hydrocarbon such as benzene, toluene or a mixture of
isomeric xylenes prior to being reacted with (A). The optimum balance between viscosity
of the reaction mixture, reaction rate and the size of the reactor required is achieved
at copolymer concentrations of from 20 to about 80%, based on the total weight of
the liquid reaction medium. Liquid aromatic hydrocarbons are preferred reaction media
because they are solvents for both (A) and (B) in addition to forming an azeotropic
mixture with any water present in the reaction mixture.
[0028] The relative amounts of (A) and (B) used to obtain the present copolymers will depend
upon the fluorine content required for the copolymer. The maximum amount of (A) that
can be reacted is limited by the hydroxyl content of (B). Preferably, at least 0.1
gram molecular weight of (A) is present for each gram molecular weight of (B). Most
preferably, from 1 to 3 gram moles of (A) is reacted with a gram molecular weight
of (B). The molecular weight of (B) is conveniently determined using gel permeation
chromatography. Preferred embodiments of (B) exhibit gram molecular weights of from
3000 to 5000 grams per mole using this method.
[0029] Reactants (A) and (B) will react in the absence of a catalyst at elevated temperatures,
however, it is generally desirable to employ one of the known acidic catalysts for
condensation reactions of hydroxyl-containing organosiloxanes. A preferred class of
catalysts includes the alkanesulfonic acids, most preferably those containing at least
one fluorine atom per molecule, such as trifluoromethanesulfonic acid. From 0.01 to
1.0% by weight of a preferred catalyst, based on the combined weights of (A) and (B)
will usually provide the level of catalytic activity required to obtain at least an
80% yield of the desired reaction product following heating of the reaction mixture
at temperatures of from 50°C to the boiling point for time periods of from 30 minutes
to several hours.
[0030] Following the reaction period, any acid present in the reaction mixture is removed.
This is conveniently accomplished by treating the reaction mixture with an amount
of a basic material to neutralize substantially all of the hydrogen halide or other
acid generated as a by-product of the reaction of (A) and (B). Basic alkali metal-
or alkaline earth metal salts such as sodium- or calcium bicarbonate are preferred.
The salt which forms is at most only slightly soluble in the reaction mixture and
is conveniently removed by filtration. The resulting filtrate contains a fluorinated
organosiloxane copolymer of this invention.
[0031] The acid-free reaction mixture may not require any additional processing other than
removal or addition of solvent if the copolymer is to be used as a coating or encapsulating
material. Other end use applications of the present copolymers, including foam stabilizers,
may require replacing at least a portion of the liquid hydrocarbon or other reaction
medium with a less volatile solvent for the copolymer. If the copolymer is to be used
to stabilize a foam produced by introducing a gaseous blowing agent into a composition
including a liquid polydimethylsiloxane in accordance with one aspect of this invention,
preferred solvents include liquid trimethylsiloxy- or hydroxyl- endblocked polydimethylsiloxanes
exhibiting viscosities of from 0.001 to about 0.1 Pa's at 25°C.
[0032] The following examples disclose preferred embodiments of copolymers prepared in accordance
with the present method and their use as polyorganosiloxane foam stabilizers. The
examples should not be interpreted as limiting the scope of this invention as defined
in the accompanying claims. All parts and percentages are by weight unless otherwise
indicated.
Example 1
[0033] Four mixtures of homologous fluorinated organosiloxane copolymers of this invention,
designated hereinafter as I, II, III and IV, were prepared by reacting a nonfluorinated
organosilane copolymer of the type described by Daudt and Tyler in Example 3 of the
aforementioned U.S. Patent No. 2,676,182 with a mixture of homologous fluorosilanes
of the general formula
F(
CF2)
nCH
2C
H2Si(CH
3)pCl
3-p where n represents 6, 8, 10 or 12, the average value of n in the mixture was 8 and
P was 0, 1 or 2. The nonfluorinated organosilane copolymer, identified hereinbefore
as reactant (B), contained (CH
3)
3SiO
1/2 units and SiO
4/2 units in a molar ratio of about 0.7:1, respectively, and 3.1% by weight of hydroxyl
groups, exhibited a molecular weight of 4200, determined by gel permeation chromatography,
and was introduced into the reaction mixture as a 75% by weight solution in isomeric
xylenes.
[0034] Three fluorosilanes, where p of the foregoing formula was 0, 1 or 2, were prepared
by reacting a mixture of homologous fluoroolefins of the general formula F(CF
2)
nCH=CH
2 with a silane of the general formula H(CH
3)
pSiCl
(3-p), where n and P are defined hereinabove.
[0035] The preparation of each of the four fluorinated copolymers is described in detail
hereinbelow:
Copolymer I - Reaction product of F(CF2)nCH2CH2Si(CH3)2Cl (A) with the organosiloxane copolymer (B) in a 1:1 molar ratio.
[0036] A sample of a mixture of homologous olefins F(CF
2)
nCH=CH
2 received from E. I. DuPont deNemours and Co. was distilled under reduced pressure
to yield a purified mixture wherein in each of the molecules n of the foregoing formula
had the value 6, 8, 10 or 12. The average molecular weight of the purified mixture,
determined from a vapor phase chromatogram was 422 g./mol. A 42.2 g. portion of the
purified mixture was reacted in a sealed glass tube with 12.3 g. of dimethylchlorosilane
and 4 drops of an isopropanol solution of chloroplatinic acid (equivalent to 1 x 10
-4 mole of platinum per mole of fluorinated olefin). The tube was heated at a temperature
of 110°C for 20 hours to yield a fluorinated silane (1). A second sample of fluorinated
silane (2) was prepared in a similar manner using 87.7 g. of the fluoroolefin, 28.4
g. of dimethylchlorosilane and 20 drops of the chloroplatinic acid solution. In this
instance the reaction mixture was heated for 2 days at 110°C. Samples (1) and (2)
were combined and distilled under reduced pressure. The distillate boiling from 92°C
at 2.9 kPa to 122°C at 0.26 kPa was collected and analyzed by vapor phase chromatography.
It was found to contain about 19% by weight of unreacted olefins. The average gram
molecular weight of the silane portion was calculated to be 522.8 g. A 22.0 g. portion
of the distillate, equivalent to 34.1 mmol, was combined with 200 g. (35.7 mmol) of
a 75% by weight xylene solution of the organosiloxane copolymer described hereinabove
in this example, 0.021 g. of trifluoromethanesulfonic acid and 200 g. of toluene.
The resultant mixture was heated for 1 hour at 60°C, at which time a 100 g. portion
was removed and neutralized using 0.13 g. of sodium bicarbonate. A 40 g. portion of
a trimethylsiloxy endblocked polydimethylsiloxane exhibiting a viscosity of 0.02 Pa's
at 25°C was then added and the resultant mixture was concentrated by heating under
the vacuum produced by a mechanical vacuum pump until the temperature of the reaction
mixture reached 100°C. The residue was a 50% by weight solution of copolymer I in
a trimethylsiloxy endblocked polydimethylsiloxane.
[0037] Copolymer I consists essentially of repeating units corresponding to the formulae
(CH
3)
3SiO
1/2, SiO
4/2, units of the average formula F(CF2)8CH2CH2Si(CH3)201/2 and silicon-bonded hydroxyl
groups. The molar ratio of the combination of (CH
3)
3SiO
1/2 and F(CF
2)
8CH
2CH
2OSi0
3/2 units to the Si0
4/2 units was within the range of from 0.7:1 to 1.1:1 and the concentration of silicon-bonded
hydroxyl groups in the copolymer was within the range from 0.4 to 4.0 weight percent,
based on the weight of the copolymer.
[0038] Copolymer II - Reaction product of F(CF
2)
nCH
2CH
2Si(CH
3)Cl
2 with the organosiloxane copolymer in a 1:1 molar ratio.
[0039] A mixture of F(CF2)nCH=CH2 homologs was distilled as described in the foregoing procedure
for Copolymer I. The distilled olefin was then combined with 8% by weight of zinc
dust and heated at about 80°C for one hour, at which time the liquid portion was distilled
under reduced pressure. The fraction boiling from 54°C at 8.4 kPa to 120°C at 4.7
kPa was collected and analyzed by vapor phase chromatography. The fraction was found
to contain 34% of F(CF2)6CH=CH2, 37% of F(CF
2)
8CH=CH
2, 22% of F(CF
2)
10CH=CH
2 and 4% of F(CF
2)
12CH=CH
2. The calculated average molecular weight of the fraction was 442. Three 64.5 g. (146
mmole) portions of this distillate were each reacted in a sealed tube with 23 g (200
mmoles) of methyldichlorosilane in the presence of 200 1 of the chloroplatinic acid
solution described in the first part of this Example. The tubes were heated for 15
hours at 115°C. The resultant products were combined and distilled under reduced pressure.
The fraction boiling from 71°C at 2.9 kPa to 150°C at 0.13 kPa was collected and analyzed
by vapor phase chromatography. The fraction amounted to an 86% yield, based on the
olefin, and exhibited an average molecular weight of 544 g/mol. The fraction was found
to contain 38% of the F(CF
2)
nCH
2CH
2Si(CH
3)Cl
2 homolog where n = 6, 35% of the n = 8 homolog, 19% of the n = 10 homolog and 4% of
the n = 12 homolog. A 20.4 g portion of this fraction, equivalent to 37.5 mmol, based
on its average molecular weight, was reacted with 200 g (35.7 mmol, based on molecular
weight of 4200) of a 75% by weight xylene solution of the nonfluorinated organosiloxane
polymer (described hereinbefore in this Example) in the presence of 100 g of toluene
and 0.1 g trifluoromethanesulfonic acid using the procedure described in the foregoing
procedure for preparing Copolymer I. A 3.0 g portion of sodium bicarbonate and 50
g of the polydimethylsiloxane exhibiting a viscosity of 0.02 Pa's were used to obtain
the final solution of Copolymer II. Volatile materials were removed by heating the
resultant mixture under the vacuum produced by a mechanical vacuum pump until the
temperature of the mixture reached 100°C.
[0040] Copolymer III - Reaction product of F(cFZ)nSi(Me)C12 with the organosiloxane copolymer
in a 3:1 molar ratio.
[0041] Copolymer III was prepared using the same procedure and reactants described hereinbefore
in connection with Copolymer II. The only difference was that 61.2 g (107 mmol) of
the fluorinated silane F(CF
2)
nCH
2CH
2Si(Me)Cl
2 was reacted with 200 g. of the organosiloxane copolymer solution.
[0042] Copolymers II and III consisted essentially of repeating units of the formulae (CH
3)
3SiO
1/2 and SiO
4/2' units of the average formula F(CF2)8CH2CH2Si(Me)O, and silicon-bonded hydroxyl groups.
The molar ratio of the combination of (CH
3)
3SiO
1/2 and F(CF
2)
8CH
2CH
2SiO
3/2 units to Si0
4/2 units was within the range of from 0.7:1 to 1.1:1 and the concentration of silicon-bonded
hydroxyl groups in the copolymer was within the range from 0.4 to 4.0 weight percent,
based on the weight of the copolymer.
[0043] Copolymer IV - Reaction product of F(CF
2)
nCH
2CH
2SiCl
3 with a nonfluorinated organosiloxane copolymer in a 1:1 molar ratio.
[0044] Two samples of the fluorinated homologous silanes F(CF
2)
nCH
2CH
2SiCl
3 were obtained as described for the preceding Copolymers I, II and III by reacting
64.5 g. (0.15 mmol) of the fluoroolefin mixture used for Copolymer II in a sealed
tube with 24.4 g. (0.18 mmol) of trichlorosilane and 200 1 of the chloroplatinic acid
solution described hereinbefore in this Example. The sealed tube was heated for 16
hours at 115°C. The two yields of products were combined and distilled under reduced
pressure. The fraction boiling from 71°C and 2.9 kPa to 135°C and 0.13 kPa was collected
and analyzed by vapor phase chromatography. The distillate represented an 83% yield,
based on starting reactants, and exhibits an average molecular weight of 573 g./mol.
A 20.4 g. (35.6 mmol) sample of the distillate was reacted with 200 g. (35.7 mmol)
of the organosiloxane copolymer solution used to prepare the copolymers I, II and
III and 0.1 g. of trifluoromethanesulfonic acid. The procedures for preparing and
isolating the final copolymer are described hereinbefore for Copolymer II. Copolymer
IV consisted essentially of the same units as Copolymers I, II and III, with the exception
that the fluorine-containing units were of the average formula F(CF
2)
8CH
2CH
2SiO
3/2-A ten weight percent solution of copolymer I, II, III or IV in a hydroxyl endblocked
polydimethylsiloxane exhibiting a viscosity of 0.08 Pa's at 25°C had a surface tension
value in contact with air of less than 2.2 x 10
4 newtons at 25°C and required less than 100% by weight of o-xylene, based on the weight
of said solution, to achieve optical clarity.
Example 2
[0045] This example demcnstrates the utility of Copolymers I - IV described in the foregoing
Example 1 as stabilizers for foams prepared by the action of a blowing agent (isobutane)
on a moisture curable polyorganosiloxane composition.
[0046] The foamable polyorganosiloxane compositions contained the following ingredients:
(1) 100 parts of a hydroxyl endblocked polydimethylsiloxane exhibiting a viscosity
of 15 Pa's,
(2) 5 parts of CH3Si[ON=C(CH3)(C2H5)]3'
(3) 5 parts of a 50% by weight solution of copolymer I, II, III or IV described •
hereinabove,
(4) 0.2 parts of dibutyltin dilaurate and
(5) 15 parts of isobutane as the blowing agent.
[0047] Ingredient (1) was placed in a Sem Kit@ tube (commercially available from Semco,
Inc., Division of Products Research and Chemical Corporation, Glendale, CA). This
device is a cylinder formed from polyethylene, resembles a tube commonly used to package
caulking compounds and incorporates a means for adding ingredients and stirring the
contents of the tube with the exclusion of atmospheric moisture.
[0048] Ingredient (1) was deaired, following which (2) and (3) were added and a cover placed
on the rear of the tube. Ingredient (4) was then introduced using a hypodermic syringe
and the resultant formulation was mixed for 3 minutes, at which time the mixture was
transferred into a conventional one-compartment aerosol can without coming into contact
with atmospheric moisture. The valve assembly was then placed on the can and the contents
of the can were degassed under reduced pressure prior to attachment of the valve assembly
to the can by crimping. Liquified isobutane (5) was then introduced through the valve
and the can was shaken by hand for 1 minute to distribute the blowing agent homogeneously
throughout the composition.
[0049] Foams were prepared by discharging a portion of the contents of the can into a small
glass cosmetic jar to a depth of about 1.3 cm. When the foam had cured, a sample of
known volume was cut out and weighed to determine density, the cell size range was
measured using a magnifying rule, and the percent collapse was calculated using the
formula [(h
i-h
f)/h
i] x 100, where h. and h
f represent, respectively, the initial height of the dispensed foam and the height
of the cured foam. The percent by volume of cured rubber present in the final foam
was as determined. All of these values are reported in the following table.
[0050] A foam prepared using the ingredients (1), (2), (4) and (5) without a foam stabilizer
collapses substantially completely shortly after being dispensed from the container.
The cured product is a rubber containing a few widely dispersed bubbles.